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Thin film with non-self-aggregating uniform heterogeneity and drug delivery systems made therefrom

a thin film, non-self-aggregating technology, applied in the direction of pharmaceutical product form change, lighting and heating apparatus, drying machines with progressive movements, etc., can solve the problems of large medication form that requires additional storage space, tablets with a tendency for inaccuracy, and many peopl

Active Publication Date: 2004-12-23
AQUESTIVE THERAPEUTICS INC
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, this form of preparing and dispensing medications has many disadvantages including that a large proportion of adjuvants that must be added to obtain a size able to be handled, that a larger medication form requires additional storage space, and that dispensing includes counting the tablets which has a tendency for inaccuracy.
In addition, many persons, estimated to be as much as 28% of the population, have difficulty swallowing tablets.
While tablets may be broken into smaller pieces or even crushed as a means of overcoming swallowing difficulties, this is not a suitable solution for many tablet or pill forms.
For example, crushing or destroying the tablet or pill form to facilitate ingestion, alone or in admixture with food, may also destroy the controlled release properties.
However, historically films and the process of making drug delivery systems therefrom have suffered from a number of unfavorable characteristics that have not allowed them to be used in practice.
Examination of films made in accordance with the process disclosed in Fuchs, however, reveals that such films suffer from the aggregation or conglomeration of particles, i.e., self-aggregation, making them inherently non-uniform.
When large dosages are involved, a small change in the dimensions of the film would lead to a large difference in the amount of active per film.
Since sheets of film are usually cut into unit doses, certain doses may therefore be devoid of or contain an insufficient amount of active for the recommended treatment.
Failure to achieve a high degree of accuracy with respect to the amount of active ingredient in the cut film can be harmful to the patient.
For this reason, dosage forms formed by processes such as Fuchs, would not likely meet the stringent standards of governmental or regulatory agencies, such as the U.S. Federal Drug Administration ("FDA"), relating to the variation of active in dosage forms.
Schmidt specifically pointed out that the methods disclosed by Fuchs did not provide a uniform film and recognized that that the creation of a non-uniform film necessarily prevents accurate dosing, which as discussed above is especially important in the pharmaceutical area.
Moreover, his process is a multi-step process that adds expense and complexity and is not practical for commercial use.
These methods have the disadvantage of requiring additional components, which translates to additional cost and manufacturing steps.
Furthermore, both methods employ the use the conventional time-consuming drying methods such as a high-temperature air-bath using a drying oven, drying tunnel, vacuum drier, or other such drying equipment.
Such processes also run the risk of exposing the active, i.e., a drug, or vitamin C, or other components to prolonged exposure to moisture and elevated temperatures, which may render it ineffective or even harmful.
In addition to the concerns associated with degradation of an active during extended exposure to moisture, the conventional drying methods themselves are unable to provide uniform films.
Uniformity is particularly difficult to achieve via conventional drying methods where a relatively thicker film, which is well-suited for the incorporation of a drug active, is desired.
Thicker uniform films are more difficult to achieve because the surfaces of the film and the inner portions of the film do not experience the same external conditions simultaneously during drying.
Thus, observation of relatively thick films made from such conventional processing shows a non-uniform structure caused by convection and intermolecular forces and requires greater than 10% moisture to remain flexible.
The amount of free moisture can often interfere over time with the drug leading to potency issues and therefore inconsistency in the final product.
The difficulty in achieving a uniform film is directly related to the Theological properties and the process of water evaporation in the film-forming composition.
The result of the repeated destruction and reformation of the film surface is observed as a "ripple effect" which produces an uneven, and therefore non-uniform film.
Frequently, depending on the polymer, a surface will seal so tightly that the remaining water is difficult to remove, leading to very long drying times, higher temperatures, and higher energy costs.
Air can be trapped in the composition during the mixing process or later during the film making process, which can leave voids in the film product as the moisture evaporates during the drying stage.
The film frequently collapse around the voids resulting in an uneven film surface and therefore, non-uniformity of the final film product.
This situation also provides a non-uniform film in that the spaces, which are not uniformly distributed, are occupying area that would otherwise be occupied by the film composition.
None of the above-mentioned patents either addresses or proposes a solution to the problems caused by air that has been introduced to the film.
The absence of a uniform thickness detrimentally affects uniformity of component distribution throughout the area of a given film.
Uncontrolled air currents, either above or below the film, can create non-uniformity in the final film products.
Further, increasing the number of particles leads to a hindered settling effect based on the solids volume fraction.
More particles suspended in the liquid phase results in decreased velocity.
The rheology requirements for the inventive compositions and films are quite severe.
Such very rapid structural recovery retards particle settling and sedimentation.
Such dried upper portions serve as a barrier to further vapor release as the portions beneath are dried, which results in non-uniform films.
Any top fluid flow, such as air, also must not overcome the inherent viscosity of the film-forming composition.
Moreover, air velocities are desirably below the yield values of the film, i.e., below any force level that can move the liquids in the film-forming compositions.
Furthermore, bottom drying also tends to result in a lower internal film temperature as compared to top drying.
Such lower internal film temperatures often result in decreased drug degradation and decreased loss of certain volatiles, such as flavors.
Films containing sensitive active components, however, may face degradation problems at high temperatures.
Degradation of an active component is typically undesirable as it may cause instability, inactivity, and / or decreased potency of the active component.
For instance, if the active component is a drug or bioactive material, this may adversely affect the safety or efficacy of the final pharmaceutical product.
Additionally, highly volatile materials will tend to be quickly released from this film upon exposure to conventional drying methods.
Moreover, temperature has a significant effect on the rate of such reactions.
Therefore, it is commonly understood that exposing an active component to high temperatures will initiate and / or accelerate undesirable degradation reactions.
Proteins from bovine extract are also known to degrade at such low temperatures.
Due to the short heat exposure and evaporative cooling, the film components such as drag or volatile actives remain unaffected by high temperatures.
In contrast, skinning on the top surface traps liquid carrier molecules of increased energy within the film, thereby causing the temperature within the film to rise and exposing active components to high, potentially deleterious temperatures.
Second, thermal mixing occurs within the film due to bottom heating and absence of surface skinning.
Pockets of heat in the film result in the formation of particle aggregates or danger areas within the film and subsequent non-uniformity.
The formation of such aggregates or agglomerations is undesirable because it leads to non-uniform films in which the active may be randomly distributed.
Such uneven distribution may lead to large differences in the amount of active per film, which is problematic from a safety and efficacy perspective.
Although the film surfaces may be exposed to a temperature above that at which the active component degrades, the film interior may not reach this temperature.
Moreover, such particles are desirably not fully encased or fully embedded into the film, but remain exposed to the surface of the film, such as in the case where the particles are partially embedded or partially encased.
Lifting of the film 42 may not only result in non-uniformity in the film or otherwise, but may also result in non-controlled processing of the film 42 as the film 42 and / or substrate 44 lift away from the processing equipment.
For example, thin films are difficult to inadvertently aspirate and provide an increased patient compliance because they need not be swallowed like a tablet.
Furthermore, thin films may not be crushed in the manner of controlled release tablets which is a problem leading to abuse of drugs such as Oxycontin.
As described above, such entrapped air may lead to non-uniform films.
In this way, simethicone reduces the surface tension of bubbles air located in the solution, such as foam bubbles, causing their collapse.

Method used

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  • Thin film with non-self-aggregating uniform heterogeneity and drug delivery systems made therefrom
  • Thin film with non-self-aggregating uniform heterogeneity and drug delivery systems made therefrom
  • Thin film with non-self-aggregating uniform heterogeneity and drug delivery systems made therefrom

Examples

Experimental program
Comparison scheme
Effect test

examples a-i

[0186] Water soluble thin film compositions of the present invention are prepared using the amounts described in Table 1.

1 TABLE 1 Weight (g) Ingredient A B C D E F G H I Hydroxypropylmethyl 1.76 1.63 32.00 3.67 32.00 cellulose Peppermint oil 0.90 1.0 1.05 8.0 2.67 Sweetener 0.15 0.15 0.22 0.10 4.6 1.53 0.15 Polyvinylpyrrolidone 0.94 1.05 7.0 2.33 Tween 80.sup.1 0.5 0.5 2.0 0.65 11.80 1.35 0.5 11.80 Simethicone.sup.2 0.2 0.2 0.15 0.30 1.80 0.21 0.2 1.80 Listerine.sup.3 83.35 83.35 Methylcellulose 6.0 Cornstarch.sup.4 1.75 Agar 1.25 Water 42.24 93.63 39.22 768.0 280.0 88.24 768.0 Loratadine.sup.5 19.219.2 Pullulan.sup.6 6.0 Ibuprofen 38.4 .sup.1Available from ICI Americas .sup.2Available from OSI .sup.3Available from Pfizer, Inc. including thymol (0.064%), eucalyptol (0.092%), methyl salicylate (0.060%), menthol (0.042%), water (up to 72.8%), alcohol (26.9%), benzoic acid, poloxamer 407, sodium benzoate, and caramel color .sup.4Available from Grain Processing Corporation as Pure Cote...

examples j-l

[0193] Thin films that have a controlled degradation time and include combinations of water soluble and water insoluble polymers and water soluble films that allow controlled release of an active are prepared using approximately the amounts described in Table 3.

3 TABLE 3 Weight (g) Ingredient J K L Hydroxypropylmethyl cellulose 1.0 1.0 Tween 80.sup.1 0.7 0.7 0.7 Water 5.0 Aquacoat ECD.sup.2 17.0 17.0 17.5 Peppermint oil 1.0 0.4 1.1 .sup.1Available from ICI Americas .sup.2A 30% by weight aqueous dispersion of ethyl cellulose available from FMC

[0194] The components of inventive compositions J-L were combined and formed into films using the methods for preparing inventive compositions A-I above. These films were also flexible, self-supporting and provided a uniform distribution of active which permits accuracy in dosing.

[0195] The uniformity of the films prepared from inventive compositions J-L may also be tested by either visual means measuring the weights of individual dosage films, ...

examples p -

Examples P-W

[0205] Compositions P-W were prepared to demonstrate the interaction among various conditions in production of films as they relate to the present invention. The ingredients in the below Table 6 were combined and formed into a film using the process parameters listed in Table 7 below, prepared in a 6 m drying tunnel designed to incorporate bottom drying of the films. Each of the examples shows the effect of different ingredient formulations and processing techniques on the resultant film products.

6 TABLE 6 Weight (g) Ingredient P Q R S T U V W Hydroxypropylmethyl cellulose 320 320 320 320 320 320 345 345 Water 1440 1440 1440 1440 1440 999 999 Sweetener 60 60 45 Mint flavor 80 80 Propylene Glycol 50 50 50 100 100 100 100 69.3 Xanthan 22 11 11.23 10 10 10 6.9 Water / Ethanol(60 / 40)1440 Orange Flavor 42

[0206]

7TABLE 7 Film Thickness Top.sup.1 Bot..sup.1 T.sup.1 Top.sup.2 (Micron) v (m / sec) v (m / sec) (.degree. C.) v (m / sec) P1 100 0 22 75 0 P2 350 0 22 75 0 P3 350 0 40 75 0 P4 ...

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Abstract

The invention relates to film products containing desired levels of active components and methods of their preparation. Desirably, the films disintegrate in water and may be formed by a controlled drying process, or other process that maintains the required uniformity of the film. Desirably, the films may be exposed to temperatures above that at which the active components typically degrade without concern for loss of the desired activity.

Description

[0001] The present application claims benefit to U.S. Provisional Application No. 60 / 443,741 filed Jan. 30, 2003, which is a continuation-in-part of PCT / US02 / 32575 filed Oct. 11, 2002, which claims priority to U.S. Application Ser. No. 10 / 074,272, filed Feb. 14, 2002 which claims priority to U.S. Provisional Application No. 60 / 328,868, filed Oct. 12, 2001 and U.S. Provisional Application No. 60 / 386,937, filed Jun. 7, 2002; PCT / US02 / 32594, filed Oct. 11, 2002, which claims priority to U.S. Provisional Application No. 60 / 414,276, filed Sep. 27, 2002, U.S. Application Ser. No. 10 / 074,272, filed Feb. 14, 2002, which claims priority to U.S. Provisional Application No. 60 / 328,868, filed Oct. 12, 2001 and U.S. Provisional Application No. 60 / 386,937, filed Jun. 7, 2002; and PCT / US02 / 32542, filed Oct. 11, 2002, which claims priority to U.S. Provisional Application No. 60 / 371,940, filed Apr. 11, 2002, U.S. Application Ser. No. 10 / 074,272, filed Feb. 14, 2002, which claims priority to U.S. Pro...

Claims

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Application Information

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IPC IPC(8): A61K9/00A61K9/70B29C48/08B29C48/91F26B13/10F26B13/20
CPCA61K9/006A61K9/7007A61J3/00F26B13/104F26B13/10B29C48/08B29C48/91B29C48/919A61P1/00
Inventor YANG, ROBERT K.FUISZ, RICHARD C.MYERS, GARY L.FUISZ, JOSEPH M.
Owner AQUESTIVE THERAPEUTICS INC
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